Compositions, Combustion Prevention Compositions, Methods for Preventing and/or Extinguishing Combustion, Combustion Prevention Systems, and Production Processes

ABSTRACT

Compositions comprising  
                 
 
are provided wherein R F  is a fluorine containing moiety comprising (CF 3 ) 2 CFCH 2 (CF 3 )CH—, (CF 3 ) 2 CFCH 2 ((CF 3 ) 2 CF)CH—, (CF 3 ) 2 CFCH 2 ((CF 3 ) 2 CH)CH—, (CF 3 ) 2 CHCH 2 ((CF 3 ) 2 CF)CH—, ((CF 3 ) 2 CFCH 2 ) 2 CH—, (CF 3 ) 2 CFCH 2 CF—, (CF 3 ) 2 CF—, (CF 3 ) 2 CH—, CF 3 —, or C n F 2n+1 —, n being an integer from 2 to 20; R 1  is F or H; R 2  comprises (CF 3 ) 2 CF—, (CF 3 ) 2 CH—, CF 3 —, F, or H; and R 3  comprises (CF 3 ) 2 CF—, (CF 3 ) 2 CH—, CF 3 —, F, or H, such compositions can produced according to processes, and utilized to prevent combustion utilizing systems.

CLAIM FOR PRIORITY

This application claims priority to U.S. Provisional Patent Application Ser. No. 60/735,717 entitled “Fire Extinguishing Agents, Methods for Preventing and/or Extinguishing Combustion, Fire Extinguishing Systems, and Production Process”, filed Nov. 10, 2005, the entirety of which is incorporated by reference herein.

TECHNICAL FIELD

The present disclosure is directed to fire extinguishing agents and systems and methods of extinguishing and/or preventing combustion, as well as, production processes. In particular aspects, R_(F)-olefin compounds are described for use in fire extinguishing and/or preventing systems. Other aspects of the present disclosure are also directed to the production of these compounds.

BACKGROUND OF THE DISCLOSURE

Certain bromine, chlorine, and iodine containing halogenated chemical agents have been used to extinguish fires. The use of iodine-containing compounds as fire extinguishing agents has been avoided primarily due to the expense of their manufacture or due to possible toxicity considerations.

Bromine-containing and chlorine-containing compounds; Halon 251 (CF₃CF₂Cl) Halon 1301 (CF₃Br), Halon 1211 (CF₂BrCl), and Halon 2402 (BrCF₂CF₂Br) have been utilized to extinguish fires, for example. Although the above-named bromine or chlorine-containing Halons have been used, these agents have been asserted by some to be capable of the destruction of the earth's protective ozone layer. Also, because the agents contain no hydrogen atoms which would permit their destruction in the troposphere, the agents may also contribute to global warming.

More recently, hydrofluorocarbons have been proposed for fire suppression. However, a disadvantage of these compounds is their relatively high global warming potential.

The present disclosure provides novel compounds, combustion prevention compositions and systems, as well as, methods for using the same to extinguish and/or prevent combustion.

SUMMARY OF THE DISCLOSURE

A composition comprising

wherein R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ is F or H; R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H.

A combustion prevention composition comprising

wherein R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ is F or H; R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H.

A combustion prevention composition comprising R_(F)—CR₁═CR₂R₃, wherein the R_(F) portion is C₃F₇ or C₃F₆, and the R₁, R₂, and R₃ portions are one or more of H, F, CF₃, and C₃F₇.

A production process comprising exposing an R_(F)-reactant to an olefinic reactant within a reaction vessel, the exposing producing and R_(F)-intermediate, wherein the R_(F)-reactant comprises at least three —CF₃ groups and the R_(F)-intermediate is a saturated compound comprising the three —CF₃ groups.

A production process comprising exposing an R_(F)-reactant to an olefinic reactant within a reaction vessel, the exposing producing and R_(F)-intermediate, wherein the R_(F)-reactant comprises at least one (CF₃)₂CH— group and the R_(F)-intermediate is a saturated compound comprising the (CF₃)₂CH— group.

A production process comprising exposing an R_(F)-reactant to an olefinic reactant within a reaction vessel, the exposing producing and R_(F)-intermediate, wherein the R_(F)-reactant comprises at least one —CF₃ group, the olefinic reactant comprises at least two —CF₃ groups, and the R_(F)-intermediate is a saturated compound comprising the one —CF₃ group of the R_(F)-reactant and the two —CF₃ groups of the olefinic reactant.

A combustion prevention process comprising providing a container housing a combustion prevention composition, the container being configured to couple to a combustion prevention composition distribution apparatus, the prevention composition comprising

wherein R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20, R₁ is F or H, R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H.

A combustion prevention system comprising a container housing a combustion prevention composition, the combustion prevention composition comprising

wherein R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1), n being an integer from 2 to 20, R₁ is F or H, R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and a composition distribution apparatus coupled to the container, the apparatus configured to distribute the combustion prevention composition.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a diagram of one embodiment of halogenated intermediate production in accordance with an aspect of the present disclosure.

FIG. 2 is a diagram of one embodiment of R_(F)-olefin product production in accordance with an aspect of the present disclosure

FIG. 3 is an illustration of an application of combustion prevention compositions in accordance with an aspect of the present disclosure.

DETAILED DESCRIPTION OF THE DISCLOSURE

Fire extinguishing compositions and methods, as well as, materials and methods for producing the same are described with reference to FIGS. 1-3. Referring to FIG. 1, a system 10 is depicted that includes a R_(F)-reactant reservoir 12 and an olefinic-reactant reservoir 14 coupled to a reaction vessel 16. System 10 can be configured with these reaction reservoirs to produce a halogenated intermediate within halogenated intermediate reservoir 20.

Reaction vessel 16 can be configured as a commercially operable reaction vessel. Such reaction vessels include those reaction vessels configured to react compounds in the liquid phase and/or in the gas phase at predetermined pressures and/or temperatures. Reaction vessel 16 can include conduits for receiving reactants from reservoirs 12 and 14, as well as, conduits for providing product to reservoir 20.

The R_(F)-reactant can include halogenated and hydrohalogenated compounds such as R_(F)X. The R_(F)— can include a moiety such as (CF₃)₂CFCH₂(CF₃)CH, (CF₃)₂CFCH₂((CF₃)₂CF)CH, (CF₃)₂CFCH₂((CF₃)₂CH)CH, (CF₃)₂CHCH₂((CF₃)₂CF)CH, ((CF₃)₂CFCH₂)₂CH, (CF₃)₂CFCH₂CF, (CF₃)₂CF—, (CF₃)₂CH— or CF₃, and/or C_(n)F_(2n+1), for example. The R_(F)— moiety can be bonded to a halogen X, such as F, Cl, Br, and/or 1. The C_(n)F_(2n+1) can have from 2-20 carbons. More particular examples of the R_(F)-reactant can include (CF₃)₂CFI, (CF₃)₂CFBr, (CF₃)₂CHBr, and/or (CF₃)₂CHI.

The R_(F)-reactant can include at least three —CF₃ groups, such as

for example. The R_(F)-reactant comprises at least one (CF₃)₂CH— group, such as

The R_(F)-reactant can be (CF₃)₂CH—X, with X being one or more elements of the periodic table of elements. According to exemplary embodiments X is a halogen or can comprise at least one halogen.

The R_(F)-reactant of reservoir 12 can be provided to reaction vessel 16 through a conduit using a pressure differential, for example, drawn under vacuum or forced under pressure. The R_(F)-reactant can also be provided alone or in combination with the olefinic-reactant of reservoir 14.

The olefinic-reactant can include ethylene and/or propene compounds such as C-2 and C-3 olefins. These compounds can include hydrofluorinated and/or hydrohalogenated compounds as well as perhalogenated and perfluorinated compounds. The olefinic reactant comprises at least one fluorine. The olefinic reactant can include one or more of —CF₂ or —CF₃ groups. The olefinic reactant can include at least two —CF₃ groups, such as

Exemplary olefinic reactants include, but are not limited to, ethylene, 3,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene, 4,4,4-trifluoro-3-(trifluoromethyl)but-1-ene, 3,3,3-trifluoroprop-1-ene, 1,1-difluoroethylene, fluoroethylene and/or perfluoroethylene. These reactants can be combined in reaction vessel 16 at a predetermined temperature in the presence of a media that can include methylene chloride and/or an aqueous solution of sodium metabisulfite from 20 to 40 (wt/wt) % to form a mixture 18.

According to another embodiment, the olefinic and R_(F)-reactants can be combined in the gas phase in the presence of substrate such as a catalyst, for example. Such gas phase reactions can include configuring vessel 16 as an Inconel® (INCO Limited Toronto, Canada) tube, such as OD=0.5″, Length 14.125″, wall thickness=0.035″ tube packed with support. The support can include activated carbon and/or catalysts such as FeCl₃, NiCl₂, CuCl₂, and/or ZnCl₂. The system can be configured to vaporize the reactants prior to the reactants entering vessel 16. Products recovered from vessel 16 can be passed through a scrubbing apparatus, then dried using an apparatus such as a Drierite® (W.A. Hammond Drierite Co. Ltd. P.O Box 460 Xenia, Ohio 45385) tube and liquefied in a dry ice/acetone trap, for example.

In addition to mixture 18, a catalyst such as a free radical initiator and/or a metal salt can be added. Such exemplary free radical initiators can include benzoyl peroxide, azobisisobutyronitrile, and/or tert-butylperoxide. Such exemplary metal salts can include salts of copper, iron, zinc, silver, and mixtures thereof. In other examples, mixture 18 can be heated in the absence of a catalyst. The R_(F)-reactant can be exposed to the olefinic reactant in the presence of a catalyst. The catalyst can include one or more of benzoyl peroxide, azobisisobutyronitrile, and/or tert-butylperoxide, for example. Typically, the mixture and catalyst can be stirred and a halogenated intermediate can be formed and separated from the mixture.

The halogenated intermediate can include, but is not limited to, R_(F)(R₂)₂C—C(R₁)₂X. The R_(F) moiety can be as previously described and R₁ and R₂ can be the same or different and can include hydrogen and/or fluorine, as well as, other halogenated moieties such as CF₃, for example. As described previously, X can be halogens such as 1, Br and/or Cl. In accordance with at least some embodiments, the R_(F)-intermediate can be a saturated compound comprising three —CF₃ groups, such as

The R_(F)-intermediate can be a saturated compound comprising at least one (CF₃)₂CH— group such as

The R_(F)-intermediate can also be a saturated compound including the one —CF₃ group of the R_(F)-reactant and the two —CF₃ groups of the olefinic reactant, such as

Exemplary conduits coupled to reservoir 20 include those conduits that can be coupled to separation devises such as a distillation apparatus. These separation devices can be configured to separate the halogenated intermediate from mixture 18.

Exemplary halogenated intermediates include those listed in Table 1 below. TABLE 1 Exemplary Halogenated Intermediates

Referring to FIG. 2, exemplary system 22 is depicted and includes a halogenated intermediate reservoir 20 and an elimination reactant reservoir 24 coupled to a reaction vessel 26. Reaction vessel 26 can be an industrial reactor configured to react organic compounds under predetermined temperatures and pressures. The reactor can be configured to include an agitating apparatus such as a mechanical stirrer. System 22 also includes an R_(F)-olefin product reservoir 30. Reservoirs 20, 24, and 30 can be coupled to vessel 26 via conduits configured to convey the halogenated intermediate, elimination reactant, and R_(F)-olefin product respectively. System 22 may be coupled to system 10 of FIG. 1.

According to exemplary embodiments, the halogenated intermediate of halogenated intermediate reservoir 20 can be combined with a media, such as methylene chloride and a phase transfer catalyst, such as a 75 percent (wt/wt) solution of methyltributylammonium chloride in water to form a mixture 28 within reaction vessel 26. The halogenated intermediates can include those halogenated intermediates described as well as listed above in Table 1, for example.

Upon forming mixture 28 within vessel 26, elimination reactant from elimination reactant reservoir 24 can be added to mixture 28. Exemplary elimination reactants include, but are not limited to 2,3,4,6,7,8,9,10-octahydropyrimido[1,2-a]azepine (DBU) and other dehydrohalogenating and/or dehalogenating reagents. Other exemplary eliminating reactants include mixtures of potassium hydroxide and water or alcohols such as methanol, and mixtures having a pH greater than 7. Additional elimination reactants that may be utilized are those reactants that can be utilized to remove a halogen selective to fluorines of a compound to form an olefin of the prior intermediate.

The R_(F)-olefin product can include, but is not limited to, the compound having the general formula R_(F)(R₂)C═C(R₃)₂. The R_(F) moiety can be as previously described and the R₂ is as previously described. The R₃ moiety can either be the same or different and can include one or more of (CF₃)₂CF, (CF₃)₂CH, CF₃, F, and/or H. In more preferred embodiments, the R_(F)-olefin product can have a R₃ moiety that is the same as the R₂ moiety. The R_(F)-olefin product can be used as a fire extinguishing agent. Dimers of R_(F)-olefins can also be produced. For example, the R_(F)-olefin perfluoroprop-1-ene may be dimerized over carbon at elevated temperatures to form 1,1,1,2,3,4,5,5,5-nonafluoro-4-(trifluoromethlyl)pent-2-ene.

According to least some embodiments, the R_(F)-olefin product is

with R_(F) being a fluorine containing moiety including (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ being F or H; R₂ including (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ including (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H. The compound

The R_(F)-olefin product is

with R_(F) being a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((C F₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20, R₁ being F or H, R₂ being (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H, and R₃ being (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H. The compound

can be

Exemplary R_(F)-olefin products are those shown in Table 2 below. TABLE 2 Exemplary R_(F)-Olefin Products

The following examples are exemplary of process conditions for producing halogenated intermediates and R_(F)-olefin products.

In accordance with scheme (1), in a 300 cc autoclave that can be equipped with mechanical stirring, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, 105.14 grams (0.36 mole) of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane (Matrix Scientific P.O. Box 25067 Columbia S.C. 92994-5067) and 10 grams (0.36 mole) of ethylene to form a mixture. The mixture can be heated to about 180° C. for about 6 hours. The mixture can be allowed to cooled to afford 105.99 grams of the crude monoadduct product (86 area % by gc) 1,1,1,2-tetrafluoro-2-(trifluoromethyl)-4-iodobutane and minor amounts of both the diadduct product 1,1,1,2-tetrafluoro-2-(trifluoromethyl)-6-iodohexane and the triadduct product 1,1,1,2-tetrafluoro-2-(trifluoromethyl)-8-iodooctane. The monoadduct product can be distilled at 56° C./96 torr. The product structure(s) can be confirmed by NMR analysis. The 1,1,1,2-tetrafluoro-2-(trifluoromethyl)-4-iodobutane can also be obtained from Matrix Scientific P.O. Box 25067 Columbia S.C. 92994-5067.

In further accordance with scheme (1) above, in a flask that can be equipped with an agitator, thermocouple, cold product trap, and an addition funnel, 64 grams (1.14 moles) of potassium hydroxide and about 240 mL of methanol can be placed to form a mixture. The mixture can then be heated to from about 45° C. to about 55° C. followed by the drop wise addition of 244.6 grams (0.75 mole) of 1,1,1,2-tetrafluoro-2-(trifluoromethyl)-4-iodobutane to form a reaction mixture. In the cold product trap can be collected, 144.8 grams of 3,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene product of about 93 percent purity by gas chromatography. The product structure can be confirmed by NMR analysis.

Referring to scheme (2) above, in a 2 L autoclave that can be equipped with a rupture disc, pressure gauge, dip tube with valve, vapor valve, cooling loop, and thermowell, 1035 grams (3.5 moles) of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane can be placed. The autoclave can be sealed with stirring at room temperature. To the 1,1,1,2,3,3,3-heptafluoro-2-iodopropane, 339 grams (3.5 mole) of 3,3,3-trifluoropropene can be fed via the dip tube to form a mixture. The mixture can be heated to about 180° C. wherein the autoclave pressure, which can be about 600 psig, can be observed to decrease. The reaction can be observed to be complete at which time the autoclave pressure stabilizes. The mixture can be collected and analyzed by gas chromatography to afford the following distribution: 10.3% of the starting material 3,3,3-trifluoropropene, 12.0% of the starting material 1,1,1,2,3,3,3-heptafluoro-2-iodopropane, 62.3% of the monoadduct product 1,1,1,2,5,5,5-heptafluoro-2-(trifluoromethyl)-4-iodopentane, and 12.4% of the diadduct product 1,1,1,2,7,7,7-heptafluoro-2,4-bis(trifluoromethyl)-6-iodoheptane.

In reference to scheme (2) above, in a flask that can be equipped with a material feeding tube coupled to a syringe pump, a thermocouple, and a simple distillation apparatus that can include a Vigureux column, a reflux condenser, thermocouple, angled vacuum connection adaptor that can be coupled to a dry ice/acetone trap, and a receiver flask, 419 grams of a 32 (wt/wt) percent KOH solution, and 9.6 grams of methyl tributylammonium chloride can be placed to form a mixture. Into the syringe pump, 215.41 grams (0.55 mole) of 1,1,1,2,5,5,5-heptafluoro-2-(trifluoromethyl)-4-iodopentane can be placed. The mixture can be heated to from about 75° C. to about 100° C. whereupon 1,1,1,2,5,5,5-heptafluoro-2-(trifluoromethyl)-4-iodopentane can be added to form a reaction mixture over a period of about 160 minutes. 1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene product can be collected in the receiver flask in concert with the addition of the starting material. The reaction mixture can be additionally heated to from about 75° C. to about 100° C. to drive the product from the reaction mixture into the receiver flask. The receiver flask can be emptied to afford 118.24 grams of 1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene product. The product structure can be confirmed by NMR analysis.

According to scheme (3) above, in a 300 cc autoclave that can be equipped with an agitator, rupture disc, pressure gauge, thermocouple, dip tube with valve, and vapor valve, 280.0 grams (1.2124 moles) of 2-bromo-1,1,1,3,3,3-hexafluoropropane (refer to scheme (25) below) and 2.9 grams (0.0198 mole) of tert-butyl peroxide can be placed to form a mixture. The reactor can be sealed and with stirring, heated to 120° C. To the mixture, ethylene can be added to form a reaction mixture until the autoclave pressure reaches about 200 psig whereupon a slight exotherm can be observed coupled with a decrease in autoclave pressure. Ethylene can be added continually until an equal molar amount with respect to the 2-bromo-1,1,1,3,3,3-hexafluoropropane has been added. The reaction mixture can be distilled to afford 131.4 grams of the 4-bromo-1,1,1-trifluoro-2-(trifluoromethyl)butane product and a minor amount of a diadduct 6-bromo-1,1,1-trifluoro-2-(trifluoromethyl)hexane. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (3) above, in a flask that can be equipped with an agitator, thermometer, addition funnel, and Vigreux column with Claisen side arm equipped with condenser, thermometer, and receiver flask, 18.6 grams (0.0718 mole) of 4-bromo-1,1,1-trifluoro-2-(trifluoromethyl)butane and 20.4 grams of methylene chloride can be placed to form a mixture. To the mixture, 18.3 grams (0.12 mole) of 2,3,4,6,7,8,9,10-octahydropyrimido[1,2-a]azepine (DBU) can be added drop wise to form a reaction mixture. The product, 4,4,4-trifluoro-3-(trifluoromethyl)but-1-ene, can be collected in the receiving flask simultaneous to the DBU addition. The reaction mixture can be heated until methylene chloride begins to collect in the receiving flask. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (4) above perfluoroprop-1-ene (Synquest Laboratories Inc. P.O. Box 309 Alachua, Fla. 32616-0309) can be dimerized in the presence of an organic solvent, a halide compound, and a crown ether in the liquid phase. In another embodiment, the dimerization can be performed by heating perfluoroprop-1-ene over carbon in the gas phase.

In accordance with scheme (5) above, in a 300 cc autoclave that can be equipped with an agitator, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, 136.0 grams (0.4596 mole) of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane and 3.2 grams (0.022 mole) of tert-butyl peroxide can be placed to form a mixture. The mixture can be heated to about 120° C. To the mixture, a sufficient amount of 1,1-difluoroethylene can be added to bring the autoclave pressure to about 150 psig and form a reaction mixture whereupon an exotherm can be observed. As the reaction proceeds, the autoclave pressure can be observed to decrease necessitating the addition of additional 1,1-difluoroethylene to the system. The total amount of 1,1-difluoroethene added to the autoclave can be about 57 grams (0.8901 mole). The reaction mixture can be distilled to afford 85.8 grams of the product 1,1,1,2,4,4-hexafluoro-2-(trifluoromethyl)-4-iodobutane and 52.5 grams of a diadduct product 1,1,1,2,4,4,6,6-octafluoro-2-(trifluoromethyl)-6-iodohexane and a minor amount of a triadduct 1,1,1,2,4,4,6,6,8,8-decafluoro-2-(trifluoromethyl)-8-iodooctane. The product structure(s) can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (5) above, in a flask that can be equipped with an agitator, thermometer, addition funnel, and Vigreux column with Claisen side arm equipped with condenser, thermometer, and receiver flask, 45.6 grams of a 30 (wt/wt) % KOH solution and 3.6 grams of methyltributylammonium chloride can be placed to form a mixture and heated to about 96° C. To the mixture, 38.1 grams (0.1058 mole) of 1,1,1,2,4,4-hexafluoro-2-(trifluoromethyl)-4-iodobutane can be added drop wise to form a reaction mixture. Immediately upon addition of the 1,1,1,2,4,4-hexafluoro-2-(trifluoromethyl)-4-iodobutane to the mixture, 1,1,3,4,4,4-hexafluoro-3-(trifluoromethyl)but-1-ene can be observed to collect in the receiver flask. The collected material can be further purified to afford 10.2 grams of the desired product 1,1,3,4,4,4-hexafluoro-3-(trifluoromethyl)but-1-ene. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (6) above, in a 300 cc autoclave that can be equipped with an agitator, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, an amount of 1,1,1,3,3,3-hexafluoro-2-iodopropane and a sufficient amount of catalyst can be placed to form a mixture. The mixture can be heated to from about 60° to about 190° C. To the mixture, a sufficient amount of 1,1-difluoroethylene can be added to form a reaction mixture. The total amount of 1,1-difluoroethylene added to the autoclave can be about the molar equivalent of 1,1,1,3,3,3-hexafluoro-2-iodopropane. The reaction mixture can be distilled to afford the product 1,1,1,4,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (6) above, in a flask that can be equipped with an agitator, thermometer, addition funnel, and Vigreux column with Claisen side arm equipped with condenser, thermometer, and receiver flask, a sufficient amount of catalyst and of a phase transfer catalyst can be placed to form a mixture and heated to from about 25° C. to about 100° C. To the mixture, an amount of 1,1,1,4,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane can be added drop wise to form a reaction mixture. Upon addition of the 1,1,1,2,4,4-hexafluoro-2-(trifluoromethyl)-4-iodobutane to the mixture, the product 1,1,4,4,4-pentafluoro-3-(trifluoromethyl)but-1-ene can be collected in the receiver flask. The product can be further purified by distillation. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (7) above, in a 300 cc autoclave that can be equipped with an agitator, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, an amount of 1,1,1,3,3,3-hexafluoro-2-iodopropane and a sufficient amount of catalyst can be placed to form a mixture. The mixture can be heated to from about 60° C. to about 190° C. To the mixture, a sufficient amount of fluoroethylene can be added to form a reaction mixture. The total amount of fluoroethylene added to the autoclave can be about the molar equivalent of 1,1,1,3,3,3-hexafluoro-2-iodopropane. The reaction mixture can be distilled to afford the product 1,1,1,4-tetrafluoro-2-(trifluoromethyl)-4-iodobutane. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (7) above, in a flask equipped with magnetic stirring, thermometer, addition funnel, and Vigreux column with Claisen side arm equipped with condenser, thermometer, and receiver flask, an amount of an elimination reactant and of a phase transfer catalyst can be placed to form a mixture and heated to from about 25° C. to about 100° C. To the mixture, an amount of 1,1,1,4-tetrafluoro-2-(trifluoromethyl)-4-iodobutane can be added drop wise to form a reaction mixture. Upon addition of the 1,1,1,4-tetrafluoro-2-(trifluoromethyl)-4-iodobutane to the mixture, the product 1,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene can be collected in the receiver flask. The product can be further purified by distillation. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (8) above, in a 300 cc autoclave that can be equipped with an agitator, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, an amount of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane and a sufficient amount of catalyst can be placed to form a mixture. The mixture can be heated to from about 60° C. to about 190° C. To the mixture, a sufficient amount of fluoroethylene can be added to form a reaction mixture. The total amount of fluoroethylene added to the autoclave can be about the molar equivalent of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane. The reaction mixture can be distilled to afford the product 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (8) above, in a flask equipped with an agitator, thermometer, addition funnel, and Vigreux column with Claisen side arm equipped with condenser, thermometer, and receiver flask, a sufficient amount of elimination reactant and of a phase transfer catalyst can be placed to form a mixture and heated to from about 25° C. to about 100° C. To the mixture, an amount of 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane can be added drop wise to form a reaction mixture. Upon addition of the 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane to the mixture, the product 1,3,4,4,4-pentafluoro-3-(trifluoromethyl)but-1-ene can be collected in the receiver flask. The product can be further purified by distillation. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (9) above, in a 300 cc autoclave that can be equipped with an agitator, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, an amount of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane and a sufficient amount of catalyst can be placed to form a mixture. The mixture can be heated to from about 60° C. to about 190° C. To the mixture, a sufficient amount of perfluoroethylene can be added to form a reaction mixture. The total amount of perfluoroethylene added to the autoclave can be about the molar equivalent of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane. The reaction mixture can be distilled to afford the product 1,1,1,2,3,3,4,4-octafluoro-2-(trifluoromethyl)-4-iodobutane. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (9) above, in a flask equipped with an agitator, thermometer, addition funnel, and Vigreux column with Claisen side arm equipped with condenser, thermometer, and receiver flask, an amount of elimination reactant and of a phase transfer catalyst can be placed to form a mixture and heated to from about 25° C. to 100° C. To the mixture, an amount of 1,1,1,2,3,3,4,4-octafluoro-2-(trifluoromethyl)-4-iodobutane can be added drop wise to form a reaction mixture. Upon addition of the 1,1,1,2,3,3,4,4-octafluoro-2-(trifluoromethyl)-4-iodobutane to the mixture, 1,1,2,3,4,4,4-heptafluoro-3-(trifluoromethyl)but-1-ene can be formed in the receiver flask. The collected material can be further purified to afford an amount of the desired product 1,1,2,3,4,4,4-heptafluoro-3-(trifluoromethyl)but-1-ene. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (10) above, in a 300 cc autoclave that can be equipped with an agitator, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, an amount of 1,1,1,3,3,3-hexafluoro-2-iodopropane and a sufficient amount of catalyst can be placed to form a mixture. The mixture can be heated to from about 60° C. to about 190° C. To the mixture, a sufficient amount of perfluoroethylene can be added to form a reaction mixture. The total amount of perfluoroethylene added to the autoclave can be about the molar equivalent of 1,1,1,3,3,3-hexafluoro-2-iodopropane. The reaction mixture can be distilled to afford the product 1,1,2,2,4,4,4-heptafluoro-2-(trifluoromethyl)-4-iodobutane. The product structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (10) above, in a flask equipped with an agitator, thermometer, addition funnel, and Vigreux column with Claisen side arm equipped with condenser, thermometer, and receiver flask, an amount of an elimination reactant and of a phase transfer catalyst can be placed to form a mixture and heated to from about 25° C. to about 100° C. To the mixture, an amount of 1,1,2,2,4,4,4-heptafluoro-2-(trifluoromethyl)-4-iodobutane can be added drop wise to form a reaction mixture. Upon addition of the 1,1,2,2,4,4,4-heptafluoro-2-(trifluoromethyl)-4-iodobutane to the mixture, the product 1,1,2,4,4,4-hexafluoro-3-(trifluoromethyl)but-1-ene can be collected in the receiver flask. The product can be further purified by distillation. The product structure can be confirmed by GC/MS and/or NMR analysis.

According to scheme (11) above, in a 300 mL stainless steel autoclave that can be equipped with an agitator, venting valve, thermocouple, rupture disk, and a pressure gauge, 25 grams (0.13 mole) of 3,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene (refer to scheme (1) above), 75 grams (0.25 mole) of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane, 0.15 grams (0.0015 mole) of copper (I) chloride, and 0.75 grams (0.012 mole) of ethanolamine can be placed to form a mixture. The mixture can be heated to about 195° C. and held for about 16 hours to afford the intermediate product 1,1,1,2,5,6,6,6-octafluoro-2,5-bis(trifluoromethyl)-3-iodohexane. The intermediate product structure can be confirmed by GC/MS and/or NMR analysis.

In further accordance with scheme (11) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, about 20 grams (0.041 mole) of 1,1,1,2,5,6,6,6-octafluoro-2,5-bis(trifluoromethyl)-3-iodohexane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,5,6,6,6-octafluoro-2,5-bis(trifluoromethyl)-3-iodohexane to the mixture, the product 1,1,1,2,5,6,6,6-octafluoro-2,5-bis(trifluoromethyl)hex-3-ene can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

Referring to scheme (12) above, in a 300 mL stainless steel autoclave that can be equipped with an agitator, venting valve, thermocouple, rupture disk, and a pressure gauge, a sufficient amount of 3,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene (refer to scheme (1) above), a sufficient amount of 1,1,1,3,3,3-hexafluoro-2-iodopropane, and a sufficient amount of a catalyst can be placed to form a mixture. The mixture can be heated to from about 60° C. to about 195° C. and held for from about 15 hours to about 21 hours, and/or about 18 hours to afford the intermediate product 1,1,1,2,5,6,6,6-octafluoro-2,5-bis(trifluoromethyl)-3-iodohexane. The intermediate product structure can be confirmed by GC/MS and/or NMR analysis.

In further reference to scheme (12) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,5,6,6,6-octafluoro-2,5-bis(trifluoromethyl)-3-iodohexane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,5,6,6,6-octafluoro-2,5-bis(trifluoromethyl)-3-iodohexane to the mixture, the product 1,1,1,2,6,6,6-heptafluoro-2,5-bis(trifluoromethyl)hex-3-ene can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

Referring to scheme (13) above, in a 300 mL stainless steel autoclave that can be equipped with an agitator, venting valve, thermocouple, rupture disk, and a pressure gauge, a sufficient amount of 4,4,4-trifluoro-3-(trifluoromethyl)but-1-ene (refer to scheme (3) above), a sufficient amount of 1,1,1,3,3,3-hexafluoro-2-iodopropane, and a sufficient amount of a catalyst can be placed to form a mixture. The mixture can be heated to from about 60° C. to about 195° C. and held for from about 15 hours to about 21 hours, and/or about 18 hours to afford the intermediate product 1,1,1,6,6,6-hexafluoro-2,5-bis(trifluoromethyl)-3-iodohexane. The intermediate product structure can be confirmed by GC/MS and/or NMR analysis.

In further reference to scheme (13) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1 1,1,1,6,6,6-hexafluoro-2,5-bis(trifluoromethyl)-3-iodohexane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,6,6,6-hexafluoro-2,5-bis(trifluoromethyl)-3-iodohexane to the mixture, the product 1,1,1,6,6,6-hexafluoro-2,5-bis(trifluoromethyl)hex-3-ene can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

In accordance with scheme (14), in a 300 cc autoclave that can be equipped with mechanical stirring, rupture disc, pressure gauge, thermowell, dip tube with valve, and a vapor valve, a sufficient amount of 1,1,1,2,2-pentafluoro-2-iodoethane (Matrix Scientific P.O. Box 25067 Columbia S.C. 92994-5067) and of ethylene can be added to form a mixture. The mixture can be heated to from about 60° C. to about 195° C. and held for from about 15 hours to about 21 hours, and/or about 18 hours. The mixture can be allowed to cool to afford the crude product 1,1,1,2,2-pentafluoro-4-iodobutane. The product can be purified by distillation and the product structure can be confirmed by NMR analysis.

In further accordance with scheme (14) above, in a flask that can be equipped with an agitator, thermocouple, cold product trap, and an addition funnel, a sufficient amount of an elimination reactant can be placed to form a mixture. The mixture can then be heated to from about 25° C. to about 100° C. followed by the drop wise addition of 1,1,1,2,2-pentafluoro-4-iodobutane to form a reaction mixture. In the cold product trap, the product 3,3,4,4,4-pentafluorobut-1-ene can be collected. The product structure can be confirmed by NMR analysis.

Referring to scheme (15) above, AlBN (9.2 g, 0.06 mole), 1,1,1,2,3,3,3-heptafluoro-2-iodopropane (1651 grams, 5.6 mole), and 293 grams of 30% (wt/wt) aqueous Na₂S₂O₅ can be placed into a 2 L pressure reactor to form a mixture. The reactor can be sealed and heated to 80° C. under autogeneous pressure. Allyl acetate (587 grams, 5.9 mole) can be slowly added to this mixture and the mixture can be stirred for an additional 4 hours. After stirring, an organic layer can be observed, removed, washed twice with H₂O, and dried with MgSO₄ to give 2212 g of 94% (area percent by gas chromatography) the R_(F)-intermediate 4,5,5,5-tetrafluoro-4-(trifluoromethyl)-2-iodopentyl acetate.

Diethylene glycol (2944 grams) and zinc powder (1330 grams) can be placed into a 5 L 5-neck flask equipped with a simple distillation apparatus to form a mixture. This mixture can be stirred and heated to 120° C. and the 4,5,5,5-tetrafluoro-4-(trifluoromethyl)-2-iodopentyl acetate (4149 grams) can be slowly added. As the 4,5,5,5-tetrafluoro-4-(trifluoromethyl)-2-iodopentyl acetate is added, the R_(F)-intermediate 4,5,5,5-tetrafluoro-4-(trifluoromethyl)pent-1-ene (2075 grams) can be flashed-off and collected in a 1 L ice trap. The contents of the ice trap can be distilled to give 4,5,5,5-tetrafluoro-4-(trifluoromethyl)pent-1-ene >99.5% (area percent by gas chromatography) (b.p. 54° C.).

Referring to scheme (16) above, 20 grams (0.095 mole) of 4,5,5,5-tetrafluoro-4-(trifluoromethyl)pent-1-ene (refer to scheme (15) above) and 28.18 grams (0.095 mole) 1,1,1,2,3,3,3-heptafluoro-2-iodopropane can be provided to a glass pressure tube to form a mixture. To the mixture, 0.51 gram of azobisisobutyronitrile (AlBN) can be added to form a reaction mixture. The reaction mixture can be heated to and maintained at about 85° C. for about 24 hours. During heating, additional AlBN can be added (0.11 grams after 3 hours and another 0.1 grams after 21 hours). The mixture can then be washed twice with H₂O to afford the product 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane and analysis via gas chromatography can yield a 56% area percent purity.

In accordance with scheme (17) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane (refer to scheme (16) above) can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane to the mixture, the product 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)hept-3-ene can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

According to scheme (18) above, into a 300 mL autoclave that can be equipped with a dip tube, thermocouple, agitator, pressure gauge, and an attachment to a reservoir containing ethylene gas, 319 grams (0.63 mole) 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane (refer to scheme (16) above) and 3 grams (0.012 mole) dibenzoyl peroxide can be added to form a mixture. The autoclave can then be sealed, evacuated, and heated to about 100° C. Ethylene gas can be added to the mixture to form a reaction mixture. The reaction mixture can be held at a pressure of about 380 psig for about four hours. The reaction mixture can then be chilled using an ice water bath and degassed. To the reaction mixture, an additional 3.0 grams (0.012 mole) dibenzoyl peroxide can be added to form a new mixture. The autoclave can then be sealed, evacuated, and heated to about 100° C. Ethylene gas can be added to the mixture to form a new reaction mixture. The new reaction mixture can be held at a pressure of about 380 psig for about four hours then chilled with an ice water bath, degassed, and opened to provide 336.5 grams of 80 (wt/wt) percent pure (by gas chromatography) 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane product. The product can be purified by vacuum distillation (b.p. 53° C./1.3 Torr) the structure confirmed by NMR analysis.

In further accordance with scheme (18) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-(2-iodoethyl)heptane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-(2-iodoethyl)heptane to the mixture, the product 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-vinylheptane can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

According to scheme (19) above, into an autoclave that can be equipped with a dip tube, thermocouple, agitator, pressure gauge, and an attachment to a reservoir containing fluoroethylene gas, an amount of 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane (refer to scheme (16) above) and a sufficient amount of catalyst can be added to form a mixture. The autoclave can then be sealed, evacuated, and heated to from about 50° C. to about 120° C. Fluoroethylene gas can be added to the mixture to form a reaction mixture. The reaction mixture can be held at a sufficient pressure for from about four hours to about 16 hours. The reaction mixture can then be chilled using an ice water bath and degassed to provide 1,1,1,2,6,7,7,7-octafluoro-4-(2-fluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane product. The product can be purified by vacuum distillation and the structure confirmed by NMR analysis.

In further accordance with scheme (19) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,6,7,7,7-octafluoro-4-(2-fluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,6,7,7,7-octafluoro-4-(2-fluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane to the mixture, the product 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-(2-fluorovinyl)heptane can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

According to scheme (20) above, into an autoclave that can be equipped with a dip tube, thermocouple, agitator, pressure gauge, and an attachment to a reservoir containing 1,1-difluoroethylene gas, an amount of 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane (refer to scheme (16) above) and an sufficient amount of catalyst can be added to form a mixture. The autoclave can then be sealed, evacuated, and heated to from about 50° C. to about 120° C. 1,1-fluoroethylene gas can be added to the mixture to form a reaction mixture. The reaction mixture can be held at a sufficient pressure for from about four hours to about 16 hours. The reaction mixture can then be chilled using an ice water bath and degassed to provide 1,1,1,2,6,7,7,7-octafluoro-4-(2,2-difluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane product. The product can be purified by vacuum distillation and the structure confirmed by NMR analysis.

In further accordance with scheme (20) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,6,7,7,7-octafluoro-4-(2,2-difluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,6,7,7,7-octafluoro-4-(2,2-difluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane to the mixture, the product 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-(2,2-difluorovinyl)heptane can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

Referring to scheme (21) above, in a 20 mL autoclave that can be equipped with an agitator, a thermocouple, and a pressure gauge, 3.42 grams (0.0087 mole) of 1,1,1,2,5,5,5-heptafluoro-2-(trifluoromethyl)-4-iodopentane (refer to scheme (2) above) and 0.034 gram (1.4×10⁻⁴ mole) of dibenzoyl peroxide to form a mixture. The autoclave can then be sealed and heated to about 95° C. whereupon ethylene gas can be delivered to the autoclave to form a reaction mixture so that a pressure of about 350 psig can be achieved. The autoclave pressure can be observed to decline over the course of the reaction and as such the ethylene gas can be continuously delivered to the autoclave so that an autoclave pressure of about 300 psig can be maintained for about one hour. Then the reaction mixture can be degassed and analyzed by gas chromatography to afford the product 1,1,1,2-tetrafluoro-2,4-bis(trifluoromethyl)-6-iodohexane having about 81.3 (wt/wt) percent purity. The product structure can be confirmed by NMR analysis.

In further accordance with scheme (21) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2-tetrafluoro-2,4-bis(trifluoromethyl)-6-iodohexane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2-tetrafluoro-2,4-bis(trifluoromethyl)-6-iodohexane to the mixture, the product 5,6,6,6-tetrafluoro-3,5-bis(trifluoromethyl)hexe-1-ene can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

Referring to scheme (22) above, in an autoclave that can be equipped with an agitator, a thermocouple, and a pressure gauge, an amount of 1,1,1,2,5,5,5-heptafluoro-2-(trifluoromethyl)-4-iodopentane (refer to scheme (2) above) and catalyst can be added to form a mixture. The autoclave can then be sealed and heated to from about 60° C. to about 195° C. whereupon fluoroethylene gas can be delivered to the autoclave to form a reaction mixture. The fluorethylene gas can be continuously delivered to the autoclave so that an autoclave pressure of about 300 psig can be maintained for from about one hour to about 16 hours. Then the reaction mixture can be degassed and analyzed by gas chromatography to afford the product 1,1,1,2,6-pentafluoro-2,4-bis(trifluoromethyl)-6-iodohexane. The product structure can be confirmed by NMR analysis.

In further accordance with scheme (22) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,6-pentafluoro-2,4-bis(trifluoromethyl)-6-iodohexane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,6-pentafluoro-2,4-bis(trifluoromethyl)-6-iodohexane to the mixture, the product 1,5,6,6,6-pentafluoro-3,5-bis(trifluoromethyl)hex-1-ene can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

Referring to scheme (23) above, in an autoclave that can be equipped with an agitator, a thermocouple, and a pressure gauge, an amount of 1,1,1,2,5,5,5-heptafluoro-2-(trifluoromethyl)-4-iodopentane (refer to scheme (2) above) and catalyst can be added to form a mixture. The autoclave can then be sealed and heated to from about 60° C. to about 195° C. whereupon 1,1-difluoroethylene gas can be delivered to the autoclave to form a reaction mixture. The 1,1-difluorethylene gas can be continuously delivered to the autoclave so that an autoclave pressure of about 300 psig can be maintained for from about one hour to about 16 hours. Then the reaction mixture can be degassed and analyzed by gas chromatography to afford the product 1,1,1,2,6,6-hexafluoro-2,4-bis(trifluoromethyl)-6-iodohexane. The product structure can be confirmed by NMR analysis.

In further accordance with scheme (23) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,6,6-hexafluoro-2,4-bis(trifluoromethyl)-6-iodohexane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,6,6-hexafluoro-2,4-bis(trifluoromethyl)-6-iodohexane to the mixture, the product 1,1,5,6,6,6-hexafluoro-3,5-bis(trifluoromethyl)hex-1-ene can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

According to scheme (24) above, into an autoclave that can be equipped with a dip tube, thermocouple, agitator, pressure gauge, and an attachment to a reservoir containing 1,1,2-trifluoroethylene gas, an amount of 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-iodoheptane (refer to scheme (16) above) and a sufficient amount of catalyst can be added to form a mixture. The autoclave can then be sealed, evacuated, and heated to from about 50° C. to about 120° C. 1,1,2-trifluoroethylene gas can be added to the mixture to form a reaction mixture. The reaction mixture can be held at a sufficient pressure for from about four hours to about 16 hours. The reaction mixture can then be chilled using an ice water bath and degassed to provide 1,1,1,2,6,7,7,7-octafluoro-4-(1,2,2-trifluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane product. The product can be purified by vacuum distillation and the structure confirmed by NMR analysis.

In further accordance with scheme (24) above, in a flask that can be equipped with an agitator, thermocouple, addition funnel, and Vigreux column with a Claisen side arm equipped with a reflux condenser, thermocouple, and a receiver flask, a sufficient amount of an elimination reactant can be placed and heated to from about 25° C. to about 100° C. To the elimination reactant, a sufficient amount of 1,1,1,2,6,7,7,7-octafluoro-4-(1,2,2-trifluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane can be added drop wise to form a mixture. Immediately upon addition of the 1,1,1,2,6,7,7,7-octafluoro-4-(1,2,2-trifluoro-2-iodoethyl)-2,6-bis(trifluoromethyl)heptane, to the mixture, the product 1,1,1,2,6,7,7,7-octafluoro-2,6-bis(trifluoromethyl)-4-(1,2,2-trifluorovinyl)heptane can be observed to collect in the receiver flask. The product can be further purified by distillation and the structure can be confirmed by GC/MS and/or NMR analysis.

According to scheme (25) above, to a 100 cc three-neck flask that can be equipped with a thermometer, a Teflon dip tube that can be connected to a supply of 1,1,1,3,3,3-hexafluoropropane, and an outlet tube that can be connected to a ½×12″ stainless steel tube reactor, liquid bromine can be placed. The flask can be warmed by an electric heating lamp to produce a vapor temperature of from about 35° C. to about 40° C. The tube reactor can be heated to from about 540° C. to about 550° C. by an electric furnace. To the flask, 28 mL/min of 1,1,1,3,3,3-hexafluoropropane gas measured by a flow meter can be bubbled through the bromine liquid via the dip tube and consequently saturated with the bromine vapor to produce a mixture. The mixture can be carried to the tube reactor via the outlet tube. As the mixture passes through the tube reactor the reaction takes place and the 2-bromo-1,1,1,3,3,3-hexafluoropropane product can be collected in an ice/water trap, washed with water and analyzed by gas chromatography, to afford the following product distribution 63 (wt/wt) % 1,1,1,3,3,3-hexafluoropropane, 34 (wt/wt) % 2-bromo-1,1,1,3,3,3-hexafluoropropane and 1.9 (wt/wt) % 2,2-dibromo-1,1,1,3,3,3-hexafluoropropane. The product can be isolated by distillation. The product structure(s) can be confirmed by GC/MS and/or NMR analysis.

Exemplary R_(F)-intermediates as well as R_(F)-olefin products can be prepared according to schemes 26 through 30 below following the general procedures described herein.

According to scheme (31) above, in a 2 L Parr reactor (316 stainless steel) that can be equipped with a rupture disc, pressure gauge, dip tube with valve, vapor valve, cooling loop, and a thermowell, 1189 grams (4.02 moles) of 1,1,1,2,3,3,3-heptafluoro-2-iodopropane and 13 grams (0.09 mole) of tert-butyl peroxide can be placed to form a mixture. The reactor can be sealed and heated to about 120° C. while stirring. An autogenous reactor pressure can be observed to be about 100 psig. To the mixture, vinyl fluoride (fluoroethene, VF) can be added to achieve and/or maintain a reactor pressure of about 200 psig to form a reaction mixture. An exotherm can be observed along with a reactor pressure drop while the temperature remained below about 150° C. The reaction can be continued until the reactor pressure stabilizes. The reactor can be vented and the contents removed to afford about 1387 grams of the crude 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane containing product mixture. The product mixture can be analyzed by gas chromatography to afford 2.6% VF, 0.8% CH3I, 84.6% 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane, 0.7% peroxide, 8.3% 1,1,1,2,4,6-hexafluoro-2-(trifluoromethyl)-6-iodohexane (not shown), and 3.0% other. Telomers, in addition to those described above, can be formed (e.g., 1,1,1,2,4,6,8-heptafluoro-2-(trifluoromethyl)-8-iodooctane, 1,1,1,2,4,6,8,10-octafluoro-2-(trifluoromethyl)-10-iododecane, etc.). The product mixture can be distilled in a 1 L flask equipped with an agitator, thermometer, and a silver-lined, vacuum jacketed column. The column can be 19.5″ long with a packed length of 13.5″ and packed with 0.16″ Monel™ (Inco Limited 145 King Street West Suite 1500 Toronto, Ontario M5H 4B7, Canada) Pro-Pake (Cannon Instrument Company, 2139 High Tech Rd., State College, Pa. 16803). The column can be equipped with a magnetic take-off head with thermometer, condenser, and receiver flask. The distillation can afford about 1205 grams of 98.5% to 99.0% (by gas chromatography) of the 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane product. The product structure can be confirmed by NMR and/or chromatographic and/or spectroscopic analysis.

In accordance with scheme (32) above, in a 2 L flask that can be equipped with an agitator, thermometer, addition funnel for the addition of 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane (refer to scheme (31) above), and a Claisen distillation head side-arm that can be equipped with a condenser at about 0° C. along with an adapter that can be equipped with a cold trap and a chilled receiver flask, 238 grams (4.24 moles) of potassium hydroxide (KOH), 670.4 grams of water and 30 grams of a 75% (wt/wt) solution of methyltributylammonium chloride in water (aliquat 175) can be placed to form a mixture. The mixture can be heated to from about 75° C. to about 80° C. To the heated mixture, 893 grams of 1,1,1,2,4-pentafluoro-2-(trifluoromethyl)-4-iodobutane can be drop wise added to form a reaction mixture. From the reaction mixture, 405 grams of 1,3,4,4,4-pentafluoro-3-(trifluoromethyl)but-1-ene can be collected from the receiver flask.

Referring to scheme (33) above, in a 600 mL autoclave that can be equipped with an agitator, thermocouple, relief valves, sample valves and a pressure gauge, about 200 mL carbon tetrachloride, 6 gram (0.11 mole) of iron powder and 6 grams (0.023 mole) of tributyl phosphate (TBP) can be added to form a mixture. The reactor can be cooled down to about −50° C. by placing the autoclave in a dry ice/acetone bath, a vacuum can be pulled. To the mixture, 3,3,3-trifluoroprop-1-ene can be added to develop an internal pressure of about 3.4 kPa to for a reaction mixture. The reaction mixture can be heated to about 105° C. thereby producing an autogenous pressure of about 7.7 kPa. The reaction mixture can be maintained at temperature for several hours during which time the reactor pressure can be observed to decrease and settle at 2.4 kPa. To the reaction mixture, additional 3,3,3-trifluoroprop-1-ene can be fed discretely several times to drive the reaction to completion. The reaction can be observed to be complete when the absence of a pressure decrease is evident. The contents of the autoclave can transferred and distilled to afford the 2,4,4,4-tetrachloro-1,1,1-trifluoro-butane product that can have a boiling point of 86° C. at 163 mmHg. The product structure can be confirmed by NMR and/or GCMS analysis.

Referring to scheme (34) above, to a reactor that can have an outside diameter of about 19 mm and a length of about by 600 mm and can be composed of an Inconel® alloy, equipped with a heater, thermocouple, product trap, and a syringe pump, a chromium comprising carbon catalyst can be added to form a reactor space. The reactor space can be heated to from about 250° C. to about 350° C. and exposed to N₂ and a HF/N₂ mixture for about 16 hours. The reactor space can be cooled and maintained at about 300° C. and about 270 mL/minute of gaseous HF and about 11.4 mL/hour of liquid 2,4,4,4-tetrachloro-1,1,1-trifluorobutane (refer to scheme (33) above) can be delivered through the syringe pump and into a pre-heater to vaporize the 2,4,4,4-tetrachloro-1,1,1-trifluorobutane to form a reaction mixture. The reaction mixture can be washed with water, dried over MgSO₄ and collected in a dry-ice condenser to afford the crude 1,1,1-4,4,4-hexafluoro-2-butene product. Distillation of the crude product yielded 99% pure product that can have a boiling point of about 8° C. The product structure can be confirmed by NMR and/or GCMS analysis.

The present disclosure also provides combustion prevention compositions which can include the R_(F)-olefin products described herein, for example, that can prevent as well as extinguish combustion through inerting and/or dilution, as well as chemical, physical and/or thermal extinguishment and/or prevention methods. Thermal extinguishing includes “cooling” a combustion. The present disclosure also provides methods of extinguishing, preventing, and/or suppressing combustion using such compounds. The combustion prevention composition can include

with; R_(F) being a fluorine containing moiety including (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ being F or H; R₂ including (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ including (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H. The combustion prevention composition can also include

with R_(F) being a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20, R₁ being F or H, R₂ being (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H, and R₃ being (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H.

The combustion prevention compositions can also include R_(F)—CR₁═CR₂R₃, with the R_(F) portion being C₃F₇ or C₃F₆, and the R₁, R₂, and R₃ portions being one or more of H, F, CF₃, and C₃F₇. R_(F)—CR₁═CR₂R₃ can be

The present disclosure further provides combustion prevention, fire extinguishing, preventing, and/or suppressing systems for delivering such fire extinguishing agents. Exemplary aspects of the present disclosure are described with reference to FIG. 3. Referring to FIG. 3, space 37 configured with a fire extinguishing system 38 is shown. System 38 includes an extinguishing agent storage vessel or container 40 contiguous with a composition distribution apparatus 42 such as an extinguishing agent dispersing nozzle.

The apparatus can be configured to distribute the combustion prevention composition within space 37. The apparatus can also be configured to provide the composition to the space automatically upon the detection of combustion within the space. The distribution apparatus can be configured to distribute the composition in substantially liquid form and/or gaseous form. The distribution apparatus can be a streaming apparatus that may be configured to distribute the composition in a substantially liquid form. The distribution apparatus may be configured to distribute the composition in substantially gaseous form, such as from a flooding apparatus.

As depicted, a combustion 44 occurs within a pan 46 on a pedestal 48. An extinguishing mixture 50 exists within space 37 as applied to the combustion to substantially extinguish the flame.

While depicted in two dimensions, space 37, for purposes of this disclosure, should be considered to have a volume determined from its dimensions (e.g. width, height, and length). While FIG. 3 illustrates a system configured for preventing combustion within a space, as illustrated, it appears to be enclosed, the application of the mixtures, systems, and/or methods of the present disclosure are not so limited. In some aspects, the present disclosure may be used to extinguish and/or prevent combustion in open spaces, as well as, confined spaces. All combustion suitable for extinguishment, suppression, and/or prevention using the mixtures of the present disclosure are at least partially surrounded by a space. The available volume of this space can be filled with agents of the present disclosure to extinguish, suppress, and/or prevent combustion. Typically, the available volume is that volume which can be occupied by a liquid or gas (i.e. that volume which fluids (gases and liquids) can exchange). Solid constructions typically are not part of the available volume.

Furthermore, FIG. 3 illustrates a single container 40. It should be understood that the combustion prevention composition can be provided to space 37 from multiple containers and the present disclosure should not be limited to mixtures, methods, and/or systems that can be provided from a single vessel nor methods or systems that utilize a single vessel. Generally, the combustion is extinguished when the extinguishing mixture is introduced from the vessel through nozzle 42 to the space. It should also be understood that while FIG. 3 illustrates a single nozzle as the distribution apparatus, multiple nozzles may be utilized and the present disclosure should not be limited to mixtures, methods, and/or systems utilizing a single nozzle.

According to an aspect of the disclosure, the combustion prevention composition can comprise, consist essentially of, and/or consist of the R_(F)-olefin product described above such as

including those R_(F)-compositions in Table 3 below. The combustion prevention composition can include

with R_(F) being a fluorine containing moiety such as (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20, R₁ is F or H; R₂ including (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ including (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H. TABLE 3 Exemplary R_(F)-Compositions

The combustion prevention composition can also comprise, consist essentially of, and/or consist of the R_(F)-composition and a suppressing additive and/or other fire extinguishing agents. The suppressing additive employed can include gases, water, and/or mixtures thereof. Exemplary gases can include nitrogen, argon, helium, carbon dioxide, and/or mixtures thereof. In an exemplary aspect, these gases can deprive fires of necessary fuels, such as oxygen. In the same or other aspects, these gases resist decomposition when exposed to combustion. In some cases, these gases are referred to as inert gases and/or propellants. An exemplary inert gas can comprise, consist essentially of, and/or consist of nitrogen. The composition distribution apparatus 38 may be configured to force the composition from the container and through a nozzle using a propellant, such as nitrogen and/or a hydrofluorocarbon.

The extinguishing mixture can include those compounds described above with reference to Table 2, and as such, they include those compounds such as R_(F)(R₂)C═C(R₃)₂. These compounds may be used alone or as admixtures with each other or as blends with other fire extinguishing agents. The agents of this invention are suitable for use in both total flooding and portable fire suppression applications. Suitable extinguishing agents for blends with the R_(F)-olefin products include CF₃CHFCF₃, CF₃CF₂CF₂H, CF₃CH₂CF₃, CF₃CHFCF₂H, CF₃CF₂H, and/or CF₃H. The olefin product, as well as, admixtures, and/or blends can be applied to space 37 at certain volume to volume percentages. It should be understood that in the % (v/v) values set forth in this description are based in space volume and refer to design concentration as adopted and described by the National Fire Protection Association in NFPA 2001 standard on clean agent fire extinguishing, 2000 edition. The equation used to calculate the concentration of extinguishing compounds has likewise been adopted by the National Fire Protection Association and is as follows: W=V/S(C/100−C) Where:

W=weight of extinguishing compound (kg)

V=volume of test space (m³)

S=a specific volume of extinguishing compound at test temperature (m³\g)

C=concentration (% (v\v)).

In particular aspects an extinguishing mixture comprising, consisting essentially of, and/or consisting of the compounds listed in Table 2 may be employed at concentrations of about 6%, and/or less than 6%, for example, as represented in Table 4 below. TABLE 4 Cup Burner Results for Extinguishment of Heptane* Agent in Space R_(F)-Composition % (v/v) 3,4,4,4-tetrafluoro-3-(trifluoromethyl)but-1-ene 5.5 1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene 5.4 1,1,1,2,3,4,5,5,5-nonafluoro-4-(trifluoromethyl)pent-2-ene 5.2 1,3,4,4,4-pentafluoro-3-(trifluoromethyl)but-1-ene 5.3 1,1,3,4,4,4-hexafluoro-3-(trifluoromethyl)but-1-ene 4.9 1,1,1-4,4,4-hexafluoro-2-butene 5.9 *Data obtained according to ISO 14520-1: 2000/Cor 1: 2002 R_(F)-compositions may be applied using conventional application techniques and methods used for Halon such as Halon 1301 and Halon 1211. Thus, these compositions may be used in total flooding combustion prevention system in which the composition is introduced to an enclosed region (e.g. a room or other enclosure) surrounding a fire in a concentration sufficient to extinguish the fire. In accordance with the present disclosure, a total flooding system apparatus, equipment, or even rooms of an enclosure may be provided with a source of an composition and appropriate piping valves and controls as to automatically and/or manually introduce an appropriate concentration in the event that a combustion should occur. Thus, the combustion prevention composition may be pressurized with nitrogen or other inert gas up to about 600 psig at ambient conditions. Alternatively, the compositions may be applied to combustion through the use of conventional portable fire extinguishing equipment.

Systems containing the olefinic agent, in accordance with this disclosure, may be conveniently pressurized at any desirable pressure up to about 600 psig at ambient conditions. Some of the applications of the olefinic agents of this disclosure are the extinguishing of liquid and gaseous fueled fires, the protection of electrical equipment, ordinary combustibles such as wood, paper, and/or textiles, hazardous solids, and the protection of computer facilities, data processing equipment, and control rooms. The novel agents according to the present disclosure can also be introduced to a fire for suppression purposes as a liquid or gas or a combination of both. This is sometimes referred to as utilizing a composition as a streaming agent. The novel compounds according to the present invention can be introduced to fires in combination with other compounds as blends. 

1. A composition comprising

wherein: R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ is F or H; R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H.
 2. The composition of claim 1 wherein

is one or more of

and isomers thereof.
 3. A combustion prevention composition comprising

wherein: R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ is F or H; R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H.
 4. The combustion prevention composition of claim 3 wherein R_(F) is C_(n)F_(2n+1) and n is an integer from 2 to
 10. 5. The combustion prevention composition of claim 3 wherein

is one or more of

n being an integer from 0 to 5,


6. A combustion prevention composition comprising R_(F)—CR₁═CR₂R₃, wherein the R_(F) portion is C₃F₇ or C₃F₆, and the R₁, R₂, and R₃ portions are one or more of H, F, CF₃, and C₃F₇.
 7. The composition of claim 6 wherein R_(F)—CR₁═CR₂R₃ is one or more of

wherein n is an integer from 0 to 5,


8. A production process comprising exposing an R_(F)-reactant to an olefinic reactant within a reaction vessel, the exposing producing and R_(F)-intermediate, wherein the R_(F)-reactant comprises at least three —CF₃ groups and the R_(F)-intermediate is a saturated compound comprising the three —CF₃ groups.
 9. The process of claim 8 further comprising exposing the R_(F)-intermediate to an eliminating reactant wherein the exposing produces an R_(F)-product, the R_(F)-product being an unsaturated compound comprising at least the three —CF₃ groups.
 10. The process of claim 8 wherein the olefinic reactant comprises at least one fluorine.
 11. The process of claim 8 wherein the olefinic reactant comprises one or more of CF₂ or CF₃.
 12. The process of claim 8 wherein the R_(F)-reactant is exposed to the olefinic reactant in the presence of an initiator.
 13. The process of claim 12 wherein the initiator comprises one or more of benzoyl peroxide, azobisisobutyronitrile, and/or tert-butylperoxide.
 14. The process of claim 8 wherein: the R_(F)-reactant is

the olefinic reactant is H₂C═CF₂; and the R_(F)-intermediate is


15. A production process comprising exposing an R_(F)-reactant to an olefinic reactant within a reaction vessel, the exposing producing and R_(F)-intermediate, wherein the R_(F)-reactant comprises at least one (CF₃)₂CH— group and the R_(F)-intermediate is a saturated compound comprising the (CF₃)₂CH— group.
 16. The process of claim 15 further comprising exposing the R_(F)-intermediate to an eliminating reactant wherein the exposing produces an R_(F)-product, the R_(F)-product being an unsaturated compound comprising at least the (CF₃)₂CH— group.
 17. The process of claim 15 wherein the R_(F)-reactant is (CF₃)₂CH—X, X being one or more elements of the periodic table of elements and the olefinic reactant comprises at least two carbons.
 18. The process of claim 17 wherein X is a halogen.
 19. The process of claim 15 wherein X comprises at least one halogen.
 20. The process of claim 15 wherein: the R_(F)-reactant is

the olefinic reactant is H₂C═CF₂; and the R_(F)-intermediate is


21. A production process comprising exposing an R_(F)-reactant to an olefinic reactant within a reaction vessel, the exposing producing and R_(F)-intermediate, wherein the R_(F)-reactant comprises at least one —CF₃ group, the olefinic reactant comprises at least two —CF₃ groups, and the R_(F)-intermediate is a saturated compound comprising the one —CF₃ group of the R_(F)-reactant and the two —CF₃ groups of the olefinic reactant.
 22. The process of claim 21 further comprising exposing the R_(F)-intermediate to an eliminating reactant wherein the exposing produces an R_(F)-product, the R_(F)-product being an unsaturated compound comprising the one —CF₃ group of the R_(F)-reactant and the two —CF₃ groups of the olefinic reactant.
 23. The process of claim 21 wherein the R_(F)-reactant is C₃F₇—X, X being one or more elements of the periodic table of elements and the olefinic reactant comprises at least two carbons.
 24. The process of claim 23 wherein X is a halogen.
 25. The process of claim 21 wherein X comprises at least one halogen.
 26. The process of claim 21 wherein: the R_(F)-reactant is

the olefinic reactant is

 and the R_(F)-intermediate is

 or isomers thereof.
 27. The process of claim 21 wherein: the R_(F)-reactant is

the olefinic reactant is

 and the R_(F)-intermediate is

 or isomers thereof.
 28. The process of claim 21 wherein: the R_(F)-reactant is

the olefinic reactant is

 and the R_(F)-intermediate is

 or isomers thereof.
 29. A combustion prevention process comprising providing a container housing a combustion prevention composition, the container being configured to couple to a combustion prevention composition distribution apparatus, the prevention composition comprising

wherein: R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ is F or H; R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H.
 30. The combustion prevention process of claim 29 wherein

is one or more of

(C_(n)F_(2n+1))CH═CF₂ and n is from 1 to 5,

wherein n is an integer from 1 to
 5. 31. The process of claim 29 wherein the distribution apparatus is configured to distribute the composition in substantially liquid form.
 32. The process of claim 31 wherein the distribution apparatus is a streaming apparatus.
 33. The process of claim 29 wherein the distribution apparatus is configured to distribute the composition in substantially gaseous form.
 34. The process of claim 29 wherein the distribution apparatus is a flooding apparatus.
 35. A combustion prevention system comprising: a container housing a combustion prevention composition, the combustion prevention composition comprising

R_(F) is a fluorine containing moiety comprising (CF₃)₂CFCH₂(CF₃)CH—, (CF₃)₂CFCH₂((CF₃)₂CF)CH—, (CF₃)₂CFCH₂((CF₃)₂CH)CH—, (CF₃)₂CHCH₂((CF₃)₂CF)CH—, ((CF₃)₂CFCH₂)₂CH—, (CF₃)₂CFCH₂CF—, (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, or C_(n)F_(2n+1)—, n being an integer from 2 to 20; R₁ is F or H; R₂ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and R₃ comprises (CF₃)₂CF—, (CF₃)₂CH—, CF₃—, F, or H; and a composition distribution apparatus coupled to the container, the apparatus configured to distribute the combustion prevention composition.
 36. The system of claim 35 wherein

is one or more of

(C_(n)F_(2n+1))CH═CF₂ and n is from 1 to 5,

wherein n is an integer from 1 to
 5. 37. The system of claim 35 wherein the composition distribution apparatus is configured to provide the composition to a space automatically upon the detection of combustion within the space.
 38. The system of claim 35 wherein the composition distribution apparatus is configured to force the composition from the container and through a nozzle using a propellant.
 39. The system of claim 38 wherein the propellant comprises nitrogen.
 40. The system of claim 38 wherein the propellant comprises a hydrofluorocarbon. 